Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D167/00—Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/0804—Manufacture of polymers containing ionic or ionogenic groups
  • C08G18/0819—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups
  • C08G18/0823—Manufacture of polymers containing ionic or ionogenic groups containing anionic or anionogenic groups containing carboxylate salt groups or groups forming them
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/08—Processes
  • C08G18/10—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
  • C08G18/12—Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step using two or more compounds having active hydrogen in the first polymerisation step
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
  • C08G18/4063—Mixtures of compounds of group C08G18/62 with other macromolecular compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/4009—Two or more macromolecular compounds not provided for in one single group of groups C08G18/42 - C08G18/64
  • C08G18/4081—Mixtures of compounds of group C08G18/64 with other macromolecular compounds
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/42—Polycondensates having carboxylic or carbonic ester groups in the main chain
  • C08G18/4263—Polycondensates having carboxylic or carbonic ester groups in the main chain containing carboxylic acid groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/62—Polymers of compounds having carbon-to-carbon double bonds
  • C08G18/6216—Polymers of alpha-beta ethylenically unsaturated carboxylic acids or of derivatives thereof
  • C08G18/625—Polymers of alpha-beta ethylenically unsaturated carboxylic acids; hydrolyzed polymers of esters of these acids
  • C08G18/6254—Polymers of alpha-beta ethylenically unsaturated carboxylic acids and of esters of these acids containing hydroxy groups
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
  • C08G18/00—Polymeric products of isocyanates or isothiocyanates
  • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
  • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
  • C08G18/40—High-molecular-weight compounds
  • C08G18/64—Macromolecular compounds not provided for by groups C08G18/42 - C08G18/63
  • C08G18/6415—Macromolecular compounds not provided for by groups C08G18/42 - C08G18/63 having nitrogen
• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
  • C09D175/00—Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
  • C09D175/04—Polyurethanes

Definitions

• Coating agent consisting of at least 3 components, process for its production and its use
• the present invention relates to a coating composition consisting of at least three components and based on a polymer containing hydroxyl and carboxyl groups and dissolved or dispersed in one or more organic solvents and a crosslinking agent containing isocyanate groups.
• the present invention also relates to a process for the production of these coating compositions and the use of the coating compositions in repair painting, for coating plastics and as a top coat or filler.
• topcoats are understood to be paints that are used to produce the top coat of paint.
• the uppermost lacquer layer can be single-layer or multi-layer, in particular two layers.
• Two-layer top coats consist of a pigmented basecoat and an unpigmented clearcoat applied to the basecoat or pigmented only with transparent pigments.
• Two-coat lacquers are now produced by the wet-on-wet process, in which a pigmented basecoat is pre-lacquered and the basecoat layer thus obtained is overcoated with a clear lacquer without a baking step and then basecoat film and
• the clear lacquer applied to the not yet hardened basecoat must not dissolve or otherwise interfere with the basecoat layer, because otherwise coatings with poor appearance are obtained.
• the top coating compositions must be able to be applied by spraying with the aid of automatic painting systems. For this purpose, they have to have such a high solids content in the case of spray viscosity that lacquer films with a sufficient layer thickness are obtained with 1 to 2 spray coats (cross coats). and they must provide baked-on paint films that have a good appearance (good flow, high gloss, little tendency to cook, good top coat and high hardness) and good weather resistance.
• EP-B-358 979 discloses aqueous two-component polyurethane coating compositions which contain a polyacrylate resin containing hydroxyl groups and a polyisocyanate component which is dispersed in water.
• these lacquers described in EP-B-358 979 show in terms of gloss, relaxation (slight scar of the coating), tendency to cook and the resulting spray safety, and in terms of
• DE-AS 25 07 884 discloses a process for the production of aqueous coating compositions, in which a solution of a carboxyl-containing polyacrylate and / or polyester is first prepared in an organic solvent, if appropriate crosslinking agents and pigments and Fillers are dispersed in the organic solution and the resulting dispersion after neutralization of the carboxyl groups of the binder is dispersed in water.
• a disadvantage of this process is that the organic solvent must be removed by azeotropic distillation after the aqueous dispersions have been prepared. This additional process step entails additional costs. Furthermore, this removal of the solvent by distillation is only possible at the manufacturer of the coating agent, but not at the customer. The finished, aqueous paints must therefore be transported and stored, which often leads to problems, particularly in the field of automotive refinishing, since very long shelf lives of at least 24 months are required there.
• Blocked polyisocyanates, epoxy resins and / or aminoplast resins are used as crosslinking agents for the production of the coating compositions described in DE-AS 25 07 884. These coating agents described there therefore only harden at elevated temperatures between 100 and 300 ° C. and are therefore not suitable for the field of refinishing.
• EP-A-368 499 discloses aqueous coating compositions which contain polyethers or polyesters containing ether groups as binders containing hydroxyl groups and amine / formaldehyde resins as crosslinking agents. These coating compositions are produced by first producing the binder and the crosslinking agent in an organic solvent. This mixture is mixed with a curing catalyst shortly before the coating agent is applied and adjusted to the desired viscosity with water.
• the present invention is therefore based on the object of providing an aqueous coating composition which has improved properties and / or provides improved coating films compared to the aqueous two-component polyurethane coating compositions known from EP-B-358 979.
• the new coating composition should ensure an improved flow, improved gloss, improved relaxation (low scar), less tendency to cook, improved spray resistance, improved filling and improved weather resistance of the resulting coatings compared to aqueous coating compositions based on aqueous acrylate copolymer dispersions .
• the new coating agent should be suitable for the field of automotive refinishing, ie it should be curable at low temperatures (generally 80 ° C.) and lead to coatings that at least meet the requirements that are usually placed on a car refinish.
• the coating agent should therefore have, for example, a good gloss (> 85 E at 20 "), a high hardness (> 110 blows) and good weather resistance (after 10 days constant climate ⁇ mlgl).
• AI at least one acrylate copolymer (AI) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, an OH number of 40 to 200 mgKOH / g and an acid number of 5 to 150 mgKOH / g and / or
• polyester resin (A2) at least one polyester resin (A2) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, an OH number of 30 to 250 mgKOH / g and an acid number of 5 to 150 mgKOH / g and / or
• (A3) at least one polyurethane resin (A3) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, an OH number of 20 to 200 mgKOH / g and an acid number of 5 to 150 mgKOH / g and
• Component (II) as crosslinking agent (F) consists of at least one non-blocked di- and / or polyisocyanate (F1), optionally dissolved or dispersed in one or more organic solvents, and optionally at least one further crosslinking agent from at least one epoxy compound (F2) with at least two epoxy groups per molecule and / or optionally at least one aminoplast resin (F3), and
• component (III) is essentially free of binder and contains water.
• the present invention also relates to a process for the production of these coating compositions and the use of the coating compositions in the repair coating, for the coating of plastics and as a topcoat or filler.
• the coating compositions according to the invention have better properties than aqueous coating compositions which contain the same binders and crosslinkers, but in which the binders according to the teaching of EP-B-358 979 as an aqueous dispersion and not as organic solution or dispersion were incorporated into the coating composition.
• the coating compositions according to the invention are distinguished by an improved gloss, improved tensioning (small scar), lower cooking inclination and therefore due to better spraying safety and improved weather resistance (condensation water constant climate test).
• coating compositions according to the invention can be prepared from the at least three components by simple mixing, without the need for expensive equipment for mixing or dispersing.
• the coating compositions according to the invention are therefore particularly suitable for
• the coating agent can be produced by the painter directly before the application of the coating agent by simply mixing the components and can be cured at low temperatures.
• the coating compositions according to the invention surprisingly lead to coatings with a high gloss, good fullness, good flow, high hardness, low tendency to cook and good weather resistance.
• the coating compositions according to the invention ensure a high degree of variability, since not only crosslinking agents, pigments and additives recommended for aqueous coating compositions can be used, but also crosslinking agents, pigments and additives which are used in conventional systems can be used.
• the coating compositions according to the invention are distinguished by very good storage stability, which corresponds to that of conventional coating compositions.
• component (I) of the coating composition according to the invention as binder (A)
• AI at least one acrylate copolymer (AI) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, an OH number of 40 to 200 mgKOH / g and an acid number of 5 to 150 mgKOH / g and / or
• polyester resin (A2) at least one polyester resin (A2) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, an OH number of 30 to 250 mgKOH / g and an acid number of 5 to 150 mgKOH / g and / or
• (A3) at least one polyurethane resin (A3) dissolved or dispersed in one or more organic, water-dilutable solvents and containing hydroxyl and carboxyl groups and having a number average molecular weight between 1,000 and 30,000, one OH number from 20 to 200 mgKOH / g and an acid number from 5 to 150 mgKOH / g and
• the binders (AI) and / or (A2) and / or (A3) and / or (A4) are selected so that a 50% solution of the binder (A) in ethoxyethyl propionate at 23 ° C. has a viscosity of less than or equal to 2.5 dPa.s, preferably less than or equal to 2.0 dPa.s.
• acrylate copolymers with the specified OH numbers, acid numbers and molecular weights are suitable as hydroxyl- and carboxyl-containing acrylate copolymers (Al).
• component (AI) are acrylate copolymers which can be obtained by polymerization in an organic solvent or a solvent mixture and in the presence of at least one polymerization initiator from
• a2) one which can be copolymerized with (al), (a3), (a4), (a5) and (a6) and is ethylenically different from (a5) unsaturated monomer which carries at least one hydroxyl group per molecule and is essentially free of carboxyl groups, or a mixture of such monomers,
• Acrylic and / or methacrylic acid which is then reacted during or after the polymerization reaction with the glycidyl ester of a monocarboxylic acid having 5 to 18 carbon atoms per molecule and branched in the ⁇ -position,
• a6) optionally an essentially carboxyl group-copolymerizable with (al), (a2), (a3), (a4), and (a5), which is different from (al), (a2), (a4) and (a5) free, ethylenically unsaturated monomer or a mixture of such monomers,
• component (a1) can be any copolymer of (a2), (a3), (a4), (a5) and (a6), essentially carboxyl-free esters of (meth) acrylic acid or a mixture of these (Meth) acrylic acid esters are used.
• alkyl acrylates and alkyl methacrylates with up to 20 carbon atoms in the alkyl radical such as methyl, ethyl, propyl, butyl, hexyl, ethylhexyl, stearyl and lauryl acrylate and methacrylate and cycloaliphatic (meth) acrylic acid esters such as cyclohexyl (meth) acrylic, isobornyl acrylate and t-butylcyclohexyl (meth) acrylic.
• Ethyltriglycol (meth) acrylate and methoxyoligoglycol (meth) acrylate with a number average molecular weight of preferably 550 or other ethoxylated and / or propoxylated hydroxyl group-free (meth) acrylic acid derivatives can also be used as component (a1).
• component (a2) with (al), (a2), (a3), (a4), (a5) and (a6) copolymerizable and different from (a5) ethylenically unsaturated monomers which have at least one hydroxyl group per molecule wear and are essentially free of carboxyl groups or a mixture of such monomers is used.
• Hydroxyalkyl esters of acrylic acid, methacrylic acid or another ⁇ , ⁇ -ethylenically unsaturated carboxylic acid are mentioned as examples. These esters can be derived from an alkylene glycol esterified with the acid, or they can be obtained by reacting the acid with an alkylene oxide.
• hydroxyalkyl esters of acrylic acid or methacrylic acid in which the hydroxyalkyl group contains up to 20 carbon atoms. contains hydrogen atoms, reaction products from cyclic esters, such as ⁇ -caprolactone and these hydroxyalkyl esters, or mixtures of these hydroxyalkyl esters or ⁇ -caprolactone-modified hydroxyalkyl esters.
• hydroxyalkyl esters examples include 2-hydroxyethyl acrylate, 2-hydroxypropyl acrylate, 3-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-hydroxypropyl methacrylate, 2-hydroxyethyl methacrylate, 4-hydroxybutyl acrylate, 4-hydroxybutyl methacrylate, hydroxystearyl acrylate and hydroxystearyl acrylate.
• esters of other unsaturated acids e.g. Ethacrylic acid, crotonic acid and similar acids with up to about 6 carbon atoms per molecule can also be used.
• olefinically unsaturated polyols can also be used as component (a2).
• Preferred polyacrylate resins (A) are obtained if at least partially trimethylolpropane monoallyl ether is used as component (a2).
• the proportion of trimethylolpropane monoallyl ether is usually 2 to 10% by weight, based on the total weight of the monomers (a1) to (a6) used to prepare the polyacrylate resin.
• the olefinically unsaturated polyols such as, in particular, trimethylolpropane monoallyl ether, can be used as the sole monomers containing hydroxyl groups, but particularly in proportion in combination with other monomers mentioned containing hydroxyl groups.
• component (a3) it is possible to use any ethylenically unsaturated monomer carrying at least one carboxyl group per molecule and copolymerizable with (al), (a2), (a4), (a5) and (a6) or a mixture of such monomers.
• Acrylic acid and / or methacrylic acid are preferably used as component (a3).
• other ethylenically unsaturated acids with up to 6 carbon atoms in the molecule can also be used.
• acids examples include ethaeryl acid, crotonic acid, maleic acid, fumaric acid and itaconic acid.
• Maleic acid mono (meth) acryloyloxyethyl ester, succinic acid mono (meth) acryloyloxyethyl ester and phthalic acid mono (meth) acryloyloxyethyl ester can also be used as component (a3).
• component (a4) one or more vinyl esters of monocarboxylic acids with 5 to 18 carbon atoms in the molecule which are branched in the ⁇ -position are used.
• the branched monocarboxylic acids can be obtained by reacting formic acid or carbon monoxide and water with olefins in the presence of a liquid, strongly acidic catalyst; the olefins can be crack products of paraffinic hydrocarbons, such as mineral oil fractions, and can contain both branched and straight-chain acyclic and / or cycloaliphatic olefins.
• olefins When such olefins are reacted with formic acid or with carbon monoxide and water, a mixture of carboxylic acids is formed in which the carboxyl groups are predominantly located on a quaternary carbon atom.
• Other olefinic starting materials are, for example, propylene tri er, propylene tetramer and diisobutylene.
• the vinyl esters can also be prepared from the acids in a manner known per se, for example by letting the acid react with acetylene. Because of the good availability, vinyl esters of saturated aliphatic mono- carboxylic acids with 9 to 11 carbon atoms, which are branched on the ⁇ -C atom, used.
• the component (a5) used is the reaction product of acrylic acid and / or methacrylic acid with the glycidyl ester of a monocarboxylic acid having 5 to 18 carbon atoms per molecule and branched in the ⁇ -position.
• Glycidyl esters of strongly branched monocarboxylic acids are available under the trade name "Cardura”.
• the reaction of acrylic or methacrylic acid with the glycidyl ester of a carboxylic acid with a tertiary ⁇ -carbon atom can take place before, during or after the polymerisation reaction.
• the reaction product of acrylic and / or methacrylic acid with the glycidyl ester of versatic acid is preferably used as component (a5). This glycidyl ester is commercially available under the name "Cardura E10".
• Component (a6) which can be copolymerized with (al), (a2), (a3), (a4) and (a5) and which is different from (al), (a2), (a3) and (a4) is essentially carboxyl - Pen-free ethylenically unsaturated monomers or mixtures of such monomers are used.
• Vinylaromatic hydrocarbons such as styrene, ⁇ -alkylstyrene and vinyltoluene, are preferably used as component (a6).
• Polysiloxane macromonomers can also be used as component (a6) in combination with other monomers suitable as component (a6).
• Polysiloxane macromonomers are suitable which have a number average molecular weight from 1,000 to 40,000, preferably from 2,000 to 10,000, and on average 0.5 to 2.5, preferably 0.5 to 1.5, ethylenically unsaturated double bonds per molecule. Suitable are, for example, those in DE-OS 38 07 571 on pages 5 to 7, which in DE-OS 37 06 095 in columns 3 to 7, that in EP-B 358 153 on pages 3 to 6 and the polysiloxane macromonomers described in US Pat. No. 4,754,014 in columns 5 to 9.
• acryloxisilane-containing vinyl monomers with the above-mentioned molecular weights and contents of ethylenically unsaturated double bonds are also suitable, for example compounds which can be prepared by reacting hydroxyl-functional silanes with epichlorohydrin and then reacting the reaction product with methacrylic acid and / or hydroxyalkyl esters of (meth) - acrylic acid.
• Polysiloxane macro monomers of the following formula are preferably used as component (a6):
• R 1 H or CH 3
• R 2 , R 3 , R 4 , R 5 identical or different aliphatic hydrocarbon radicals with 1 to 8
• the ⁇ , ⁇ -acryloxyorganofunctional polydimethylsiloxane of the formula is particularly preferred
• n '9 a Acryloxyäquivalent of 550 g per ⁇ qui ⁇ valent, an OH number of 102 mg KOH / g and a Visko ⁇ intensity of 240 mPa * s (25 C ⁇ ) are used.
• polysiloxane macromonomers suitable as component (a6) are also the compounds mentioned in the international patent application with publication number WO 92/22615 on page 12, line 18, to page 18, line 10.
• the amount of the polysiloxane macromonomer (a6) used for modifying the acrylate copolymers (AI) is less than 5% by weight, preferably 0.05 to 2.5% by weight, particularly preferably 0.05 to 0.8% by weight. %, each based on the total weight of the monomers used to prepare the copolymer (AI).
• the type and amount of components (a1) to (a6) is selected so that the polyacrylate resin (AI) has the desired OH number, acid number and glass transition temperature.
• Acrylate resins used with particular preference are obtained by polymerizing
• component (a2) 10 to 40% by weight, preferably 15 to 35% by weight, of component (a2), (a3) 1 to 15% by weight, preferably 2 to 8% by weight, of component (a3),
• component (a4) 0 to 25% by weight, preferably 5 to 15% by weight, of component (a4),
• component (a5) 0 to 25% by weight, preferably 5 to 15% by weight, of component (a5) and
• component (a6) 5 to 30% by weight, preferably 10 to 20% by weight, of component (a6),
• the polyacrylate resins (AI) used according to the invention are prepared in an organic solvent or solvent mixture and in the presence of at least one polymerization initiator.
• the organic solvents and polymerization initiators used are the solvents and polymerization initiators customary for the production of polyacrylate resins and suitable for the production of aqueous dispersions.
• solvents examples include butyl glycol, 2-methoxypropanol, n-butanol, methoxybutanol, n-propanol, ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, diethylene glycol monomethyl ether, diethylene glycol monoethyl ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether, diethylene glycol ethylene glycol ether and
• AI polyacrylate resins
• Free-radical initiators such as e.g. called t-butyl perethyl hexanoate, benzoyl peroxide, azobisisobutyronitrile and t-butyl perbenzoate.
• the initiators are preferably used in an amount of 2 to 25% by weight, particularly preferably 4 to 10% by weight, based on the total weight of the monomers.
• the polymerization is expediently carried out at a temperature of 80 to 160 ° C., preferably 110 to 160 ° C.
• Ethoxyethyl propionate and isopropoxypropanol are preferably used as solvents.
• the polyacrylate resin (Al) is preferably produced by a two-stage process, since the resulting aqueous coating compositions have better processability.
• Polyacrylate resins which can be obtained by
• the polyacrylate resin obtained is optionally at least partially neutralized.
• components (a4) and / or (a5) together with at least part of the solvent and to meter in the remaining components.
• the components (a4) and / or (a5) can only be partially added to the initial charge together with at least part of the solvent, and the rest of these components can be added as described above. For example, at least 20% by weight of the solvent and about 10% by weight of components (a4) and (a5) and, if appropriate, parts of components (a1) and (a6) are preferably introduced.
• the amount and rate of addition of the initiator is preferably chosen so that a polyacrylate resin (Al) with a number average molecular weight of 1000 to 30,000 is obtained. It is preferred that with the
• Initiator feed is started some time, generally about 15 minutes, before the feed of the monomers.
• a method is further preferred in which the initiator addition begins at the same time as the addition of the monomers and is ended about half an hour after the addition of the monomers has ended.
• the initia Tor is preferably added in a constant amount per unit of time. After the addition of initiator has ended, the reaction mixture is kept at the polymerization temperature (as a rule 1 1/2 h) until all of the monomers used have essentially been completely reacted.
• Substantially completely converted is intended to mean that preferably 100% by weight of the monomers used have been reacted, but it is also possible for a low residual monomer content of at most up to about 0.5% by weight, based to the weight of the reaction mixture, unreacted.
• the monomers for the preparation of the polyacrylate resins (Al) are preferably polymerized in the case of a not too high polymerization solid, preferably a polymerization solid of 70 to 50% by weight, and then the solvents are partially removed by distillation, so that the resultant Polyacrylate resin solutions have a solids content of preferably 80 to 60% by weight.
• component (A2) are polyesters which can be obtained by reacting
• pl polycarboxylic acids or their esterifiable derivatives, optionally together with monocarboxylic acids, p2) polyols, possibly together with monools,
• Aromatic, aliphatic and cycloaliphatic polycarboxylic acids may be mentioned as examples of polycarboxylic acids which can be used as component (p1). Aromatic and / or aliphatic polycarboxylic acids are preferably used as component (p1).
• Suitable polycarboxylic acids are phthalic acid, isophthalic acid, terephthalic acid, halophthalic acids, such as tetrachloro- or tetrabromophthalic acid, adipic acid, glutaric acid, azelaic acid, sebacic acid, fumaric acid, maleic acid, trimellitic acid, pyromellitic acid, tetrahydrophthalic acid, hexahydrophthalic acid, tetrahydrophthalic acid,
• Cyclobutanetetracarboxylic acid and others The cycloaliphatic polycarboxylic acids can be used both in their ice and in their trans form and as a mixture of both forms. Also suitable are the esterifiable derivatives of the abovementioned polycarboxylic acids, such as, for example, their mono- or polyvalent esters with aliphatic alcohols with 1 to 4 carbon atoms or hydroxy alcohols with 1 to 4 carbon atoms. In addition, the anhydrides of the above acids can also be used if they exist. If appropriate, monocarboxylic acids, such as, for example, benzoic acid, tert can also be used together with the polycarboxylic acids. Butylbenzoic acid, lauric acid, isononanoic acid and fatty acids from naturally occurring oils. Isononanoic acid is preferably used as the monocarboxylic acid.
• Suitable alcohol components (p2) for the preparation of polyester (A2) are polyhydric alcohols such as ethylene glycol, propanediols, butanediols, hexanediols, Hydroxypivalinklareneopentylester, neopentyl glycol, diethylene glycol, cyclohexanediol, cyclohexanedimethanol, trimethylpentanediol, ethylbutylpropanediol, lolpropan Ditrimethy-, trimethylolethane, trimethylolpropane, glycerol rin , Pentaerythritol, dipentaerythritol, trishydroxyethyl isocyanate, polyethylene glycol, polypropylene glycol, optionally together with monohydric alcohols, such as butanol, octanol, lauryl alcohol, ethoxylated or propoxyl
• Compounds which have a group which is reactive toward the functional groups of the polyester are particularly suitable as component (p3) for the preparation of the polyesters (A2), with the exception of the compounds mentioned as component (p4).
• the modifying component (p3) used is preferably polyisocyanates and / or diepoxide compounds, if appropriate also monoisocyanates and / or monoepoxide compounds. Suitable components (p3) are described, for example, in DE-A-40 24 204 on page 4, lines 4 to 9.
• Suitable components (p4) for the preparation of the polyesters (A2) are compounds which, in addition to a group which is reactive toward the functional groups of the polyester (A2), also have a tertiary amino group, for example monoisocyanates with at least one tertiary amino group or mercapto compounds with at least one tertiary amino group.
• a tertiary amino group for example monoisocyanates with at least one tertiary amino group or mercapto compounds with at least one tertiary amino group.
• polyesters (A2) are prepared by the known esterification methods, as described, for example, in DE-A-40 24 204, page 4, lines 50 to 65.
• the reaction is usually carried out at temperatures between 180 and 280 ° C, optionally in the presence of a suitable esterification catalyst, such as e.g. Lithium octoate, dibutyltin oxide, dibutyltin dilaurate, para-toluenesulfonic acid and the like. a ..
• the polyesters (A2) are usually prepared in the presence of small amounts of a suitable solvent as entrainer.
• a suitable solvent as entrainer.
• a suitable solvent as entrainer.
• aromatic hydrocarbons such as in particular xylene and (cyclo) aliphatic hydrocarbons
• z. B. cyclohexane used.
• polyesters which have been prepared by a two-stage process, in which firstly a polyester containing hydroxyl groups with an OH number of 100 to 300 mgKOH / g, an acid number of less than 10 mgKOH / g and a number average molecular weight of 500 to 2,000 is produced, which is then reacted in a second stage with carboxylic acid anhydrides to the desired polyester (A2).
• the amount of carboxylic anhydrides is chosen so that the polyester obtained has the desired acid number.
• acid anhydrides such as eg hexahydrophthalic anhydride, trimellitic anhydride, pyromillitic anhydride, phthalic anhydride, tetrahydrophthalic anhydride, succinic anhydride and mixtures of these and / or other anhydrides and in particular anhyrides of aromatic polycarboxylic acids, such as trimellitic anhydride, are suitable.
• the polyacrylate resin (AI) has been produced at least partially in the presence of the polyester (A2). In this case, advantageously at least 20% by weight and particularly advantageously 40 to 80% by weight of component (AI) are prepared in the presence of component (A2). Any remaining amount of component (AI) is then added to the binder solution. It is possible that this already polymerized resin has the same monomer composition as the polyacrylate resin built up in the presence of the polyester. However, a hydroxyl-containing polyacrylate resin with a different monomer composition can also be added. It is also possible to add a mixture of different polyacrylate resins and / or polyesters, a resin possibly having the same monomer composition as the polyacrylate resin built up in the presence of the polyester.
• polyurethane resins with the stated OH numbers, acid numbers and molecular numbers are suitable as the hydroxyl- and carboxyl group-containing polyurethane resin (A3).
• Suitable polyurethane resins are described, for example, in the following documents: EP-A-355 433, DE-A- 35 45 618, DE-A-38 13 866.
• Component (I) preferably uses polyurethane resins which can be prepared by reacting prepolymers containing isocyanate groups with compounds which are reactive toward isocyanate groups.
• Prepolymers containing isocyanate groups can be prepared by reacting polyols having a hydroxyl number of 10 to 1800, preferably 50 to 1200 mg KOH / g, with excess polyisocyanates at temperatures of up to 150 ° C., preferably 50 to 130 ° C, in organic solvents that cannot react with isocyanates.
• the equivalent ratio of NCO to OH groups is between 2.0: 1.0 and> 1.0: 1.0, preferably between 1.4: 1 and 1.1: 1.
• the polyols used to prepare the prepolymer can be of low molecular weight and / or of high molecular weight and contain inert anionic groups or groups capable of forming anions. It is also possible to use low molecular weight polyols with a molecular weight of 60 to 400 for the preparation of the prepolymers containing isocyanate groups. Quantities of up to 30% by weight of the total polyol constituents, preferably about 2 to 20% by weight, are used.
• a high proportion of a predominantly linear polyol with a preferred OH number of 30 to 150 mg KOH / g should be added.
• Up to 97% by weight of the total polyol can be made from saturated and unsaturated poly esters and / or polyethers with a molecular weight Mn of 400 to 5000 exist.
• the selected polyether diols should not introduce excessive amounts of ether groups, because otherwise the polymers formed will swell in water.
• Polyester diols are produced by esterification of organic dicarboxylic acids or their anhydrides with organic diols or are derived from a hydroxy carboxylic acid or a lactone. In order to produce branched polyester polyols, polyols or polycarboxylic acids with a higher valency can be used to a small extent.
• the alcohol component used to prepare the polyurethane resins preferably consists at least to a certain extent
• R 1 and R 2 each represent the same or different radical and represent an alkyl radical having 1 to 18 carbon atoms, an aryl radical or a cycloaliphatic radical, with the proviso that R 1 and / or R must not be methyl, and or
• R 3 , R 4 , Rg and R 7 each represent the same or different radicals and represent an alkyl radical with 1 to 6 C atoms, a cycloalkyl radical or an aryl radical and R 5 is an alkyl radical with 1 to 6 C atoms represents an aryl radical or an unsaturated alkyl radical having 1 to 6 carbon atoms, and n is either 0 or 1.
• All propanediols of the formula (I) in which either R ⁇ or R 2 or R ] _ and R 2 are not the same methyl are suitable as component a ⁇ ), such as 2-butyl-2-ethylpropanediol-1,3 , 2-phenyl-2-methylpropanediol-1,3, 2-propyl-2-ethylpropanediol-1,3,2-di-tert-butylpropanediol-1,3,2-butyl-2-propylpropanediol-1,3 3, 1-dihydroxymethyl-bicyclo [2.2.1] heptane, 2,2-diethylpropanediol-1,3, 2,2-dipropylpropanediol-1,3, 3,2-cyclohexyl-2-methylpropanediol-1,3 and other.
• component (a 2 ) for example, 2,5-dimethyl-hexanediol-2,5, 2,5-diethylhexanediol-2,5, 2-ethyl-5-methylhexanediol-2,5, 2,4-dimethylpentanediol-2, 4, 2,3-dimethylbutanediol-2,3, 1,4- (2 • hydroxypropyl) benzene and 1,3- (2 'hydroxypropyl) benzene can be used.
• component (a ⁇ ) are 2-propyl-2-ethyl-propanediol-1,3, 2,2-diethyl-propanediol-1,3, 3,2-butyl-2-ethyl-propanediol-1,3 and 2-phenyl-2- ethyl-propanediol-1, 3 and 2,3-dimethyl-butanediol-2,3 and 2,5-dimethylhexanediol-2,5 as component (a 2 ).
• Particularly preferred as component (a ⁇ ) are 2-butyl-2-ethyl-propanediol-1,3 and 2-phenyl-2-ethyl-propanediol-1,3 29
• Components (a ⁇ ) and / or (a 2 ) are usually used in an amount of 0.5 to 15% by weight, preferably 1 to 7% by weight, in each case based on the total weight of those used to prepare the Polyurethane resins used construction components.
• Aliphatic, cycloaliphatic and / or aromatic polyisocyanates with at least two isocyanate groups per molecule are used as typical multifunctional isocyanates for the production of the polyurethane resins.
• the isomers or isomer mixtures of organic diisocyanates are preferred. Because of their good resistance to ultraviolet light
• (Cyclo) aliphatic diisocyanates Products with a low tendency to yellowing.
• the polyisocyanate component used to form the prepolymer can also contain a proportion of higher-quality polyisocyanates, provided that this does not cause gel formation.
• Products which have been found to be suitable as triisocyanates are those which result from the trimerization or oligomerization of diisocyanates or from the reaction of diisocyanates with compounds containing polyfunctional OH or NH groups.
• the average functionality can optionally be reduced by adding monoisocyanates.
• polyisocyanates examples include phenylene diisocyanate, toluene diisocyanate, xylylene diisocyanate, bisphenylene, cyanate Naphtylendiiso-, diphenylmethane diisocyanate isophorone, Cyclobutandiisocyanat cyclopentylene, cyclohexylene, methylcyclohexylenediisocyanate, dicyclohexylmethane, ethylene, tri- diisocyanate, tetramethylene diisocyanate, hexamethylene pentamethyl-, hexamethylene diisocyanate, Propylendi - called isocyanate, ethyl ethylene diisocyanate and trimethylhexane diisocyanate.
• diisocyanates of the general formula (III) are used to prepare high-solids polyurethane resin solutions.
• X is a divalent, aromatic hydrocarbon radical, preferably a halogen, methyl or methoxy-substituted naphthylene, diphenylene or 1,2-, 1,3- or 1,4-phenylene radical, particularly are preferably a 1,3-phenylene radical and R ⁇ and R are an alkyl radical having 1-4 carbon atoms, preferably a methyl radical.
• Diisocyanates of the formula (III) are known (their preparation is described, for example, in EP-A-101 832, US Pat. No. 3,290,350, US Pat. No. 4,130,577 and US Pat. No.
• Polyurethanes are generally not compatible with water unless special components are incorporated in their synthesis and / or special production steps are carried out.
• compounds which contain two H-active groups which react with isocyanate groups and at least one group which ensures water dispersibility can be used to prepare the polyurethane resins. Suitable These groups are nonionic groups (eg polyethers), anionic groups, mixtures of these two groups or cationic groups.
• an acid number can be built into the polyurethane resin that the neutralized product can be stably dispersed in water.
• compounds which contain at least one group which is reactive towards isocyanate groups and at least one group capable of forming anions.
• Suitable groups reactive toward isocyanate groups are, in particular, hydroxyl groups and primary and / or secondary amino groups.
• Groups that are capable of forming anions are carboxyl, sulfonic acid and / or phosphonic acid groups.
• Alkanoic acids with two substituents on the ⁇ -carbon atom are preferably used.
• the substituent can be a hydroxyl group, an alkyl group or an alkylol group.
• polyols have at least one, generally 1 to 3 carboxyl groups in the molecule. They have two to about 25, preferably 3 to 10, carbon atoms.
• the polyol containing carboxyl groups can make up 3 to 100% by weight, preferably 5 to 50% by weight, of the total polyol component in the NCO prepolymer.
• the amount of ionizable carboxyl groups available as a result of the carboxyl group neutralization in salt form is generally at least 0.4% by weight, preferably at least 0.7% by weight, based on the solid.
• the upper limit is about 12% by weight.
• the amount of dihydroxyalkanoic acids in the unneutralized prepolymer gives an acid number of at least 5, preferably at least 10. At very low acid numbers, further measures are generally necessary to achieve water dispersibility.
• the upper limit of the acid number is 150, preferably 40 mg KOH / g, based on the solid.
• the acid number is preferably in the range from 20 to 40 mg KOH / g.
• the isocyanate groups of the prepolymer containing isocyanate groups are reacted with a modifier.
• the modifier is preferably added in an amount such that chain lengthening and thus molecular weight increases occur.
• Organic compounds which contain hydroxyl and / or secondary and / or primary amino groups, in particular di-, tri- and / or higher-functional polyols, are preferably used as modifiers.
• Trimethylolpropane, 1,3,4 butanetriol, glycerin, erythritol, mesoerythritol, arabitol, adonite etc. are mentioned as examples of polyols which can be used.
• Trimethylolpropane is preferably used.
• a prepolymer having isocyanate groups is preferably first prepared, from which the desired polyurethane resin is then produced by further reaction, preferably chain extension.
• Components (a), (b), (c) and (d) are implemented using the well-known methods of organic chemistry (cf., for example, Kunststoff-Handbuch, Volume 7: Polyurethane, edited by Dr. Y. Oertel, Karl-Hanser-Verlag, Kunststoff, Vienna 1983), preferably a gradual implementation of the components (e.g. formation of a first
• components (a), (b), (c) and (d) can also be reacted simultaneously.
• Examples for the production of the pre- polymers are described in DE-OS 26 24 442 and DE-OS 32 10 051.
• a simultaneous reaction of components (a), (b), (c), (d) and (e) is also possible for the production of the polyurethane resins.
• the polyurethane resins can be prepared by the known processes (for example acetone processes).
• components (a), (b), (c) and (d) are preferably reacted in ethoxyethyl propionate (EEP) as the solvent.
• EEP ethoxyethyl propionate
• the amount of ethoxyethyl propionate can vary within wide limits and should be sufficient to form a prepolymer solution with a suitable viscosity. In general, up to 70% by weight, preferably 5 to 50% by weight and particularly preferably less than 20% by weight, of solvent, based on the solid, are used.
• the reaction can very particularly preferably be carried out with a solvent content of 10-15% by weight of EEP, based on the solid.
• the reaction of components (a), (b), (c) and (d) can optionally be carried out in the presence of a catalyst such as organotin compounds and / or tertiary amines.
• a catalyst such as organotin compounds and / or tertiary amines.
• the amounts of components (a), (b), (c) and (d) are chosen so that the equivalent ratio of NCO to OH groups is between 2.0: 1.0 and> 1.0 : 1.0, preferably between 1.4: 1 and 1.1: 1.
• the NCO prepolymer contains at least about 0.5% by weight of isocyanate groups, preferably at least 1% by weight of NCO, based on the solid.
• the upper limit is approximately 15% by weight, preferably 10% by weight, particularly preferably 5% by weight, of NCO.
• Suitable as component (A4) are all water-compatible with the other components of component (I).
• dilutable binders for example acrylated polyurethane resins and / or polyester acrylates.
• Component (I) preferably contains as binder (A)
• AI at least 50% by weight, preferably at least 80% by weight, of at least one acrylate copolymer (AI),
• (A2) 0 to 30% by weight, preferably 5 to 20% by weight, of at least one polyester (A2),
• Component (I) can contain, as constituent (B), all pigments customary in coating. Both the pigments customary in aqueous coating compositions which do not react with water or which do not dissolve in water, and the pigments customarily used in conventional coating compositions can be used.
• the pigments can consist of inorganic or organic compounds and can give effects and / or color.
• the coating agent according to the invention therefore ensures, because of this large number of suitable pigments, that the coating agents can be used universally and enables a multitude of color tones to be achieved.
• Metal pigments such as commercially available aluminum bronzes, aluminum bronzes chromated according to DE-A-36 36 183 and commercially available stainless steel bronzes as well as non-metallic effect pigments such as pearlescent or interference pigments can be used as effect pigments.
• suitable inorganic color pigments are titanium dioxide, iron oxides, Sicotrans yellow and carbon black.
• suitable organic coloring pigments are indanthrene blue, cromophthal red, irgazin orange and heliogen green.
• component (I) contains at least one organic, water-dilutable solvent and optionally further solvents.
• suitable solvents are, in particular, water-miscible solvents, such as e.g. Alcohols, esters, ketones, keto esters, glycol ether esters etc. Esters, alcohols and glycol ethers are preferably used, particularly preferably ethoxyethyl propionate and isopropoxypropanol.
• component (I) contains at least one neutralizing agent.
• suitable neutralizing agents are ammonia and amines, such as e.g. Trimethylamine, triethylamine, tributylamine, dimethylaniline, diethylaniline, triphenylamine, dimethylethanolamine, diethylethanolamine, methyldiethanolamine, triethanolamine and the like.
• the neutralization can take place in the organic phase or in the aqueous phase.
• Dimethylethanolamine is preferably used as the neutralizing agent.
• the total amount of neutralizing agent used in the coating agent according to the invention is selected so that 1 to 100 equivalents, preferably 50 to 90 equivalents, of the carboxyl groups of the binder (A) are neutralized.
• the neutralizing agent can be added to component (I) and / or (II) and / or (III) and / or (IV). However, the neutralizing agent is preferably added either to component (I) and / or (III).
• component (E) can contain at least one rheology-controlling additive.
• rheology-controlling additives are: crosslinked polymeric microparticles, as disclosed, for example, in EP-A-38127, inorganic layered silicates, such as e.g.
• Inorganic layered silicates are preferably used as rheology-controlling additives.
• the inorganic sheet silicate is contained exclusively in the paint component (III).
• Component (I) may also contain at least one other customary paint additive.
• additives are defoamers, dispersing aids, emulsifiers and leveling aids.
• the additives mentioned can also be added separately to the coating agent. In this case, the additives are then referred to as component (IV).
• the lacquer component (II) as the crosslinking agent is selected from at least one non-blocked di- and / or polyisocyanate (F1) which is optionally dissolved or dispersed in one or more organic, water-dilutable solvents and, if appropriate, at least one further crosslinking agent at least one epoxy compound (F2) with at least two epoxy groups per molecule and / or at least one Amino ⁇ resin (F3) contains.
• the polyisocyanate component (F1) is any organic polyisocyanate with aliphatic, cycloaliphatic, araliphatic and / or aromatically bound free isocyanate groups.
• Polyisocyanates with 2 to 5 isocyanate groups per molecule and with viscosities of 100 to 2000 mPas (at 23 ° C.) are preferably used.
• small amounts of organic solvent, preferably 1 to 25% by weight, based on pure polyisocyanate can be added to the polyisocyanates in order to improve the incorporation of the isocyanate and, if appropriate, the viscosity of the polyisocyanate to one Lower value within the above ranges.
• Solvents suitable as additives for the polyisocyanates are, for example, ethoxyethyl propionate, butyl acetate and the like.
• isocyanates are, for example, in "Methods of Organic Chemistry", Houben-Weyl, Volume 14/2, 4th Edition, Georg Thieme Verlag, Stuttgart 1963, pages 61 to 70, and by W. Siefken, Liebigs Ann. Chem. 562, 75 to 136.
• isocyanates mentioned in the description of the polyurethane resins (A3) are suitable.
• isocyanurate groups and / or biuret groups and / or allophanate groups and / or urethane groups and / or polyisocyanates containing urea groups are obtained, for example, by reacting some of the isocyanate groups with polyols, such as, for example, trimethylolpropane and glycerol.
• Aliphatic or cycloaliphatic polyisocyanates in particular hexamethylene diisocyanate, dimerized and trimerized hexamethylene diisocyanate, isophorone diisocyanate, dicyclohexylmethane-2,4'-diisocyanate or dicyclohexylmethane-4,4'-diisocyanate or mixtures of these polyisocyanates are preferably used.
• the polyisocyanate component (B) can also consist of any mixtures of the polyisocyanates mentioned by way of example.
• the polyisocyanate component (F1) is advantageously used in the coating compositions according to the invention in an amount of at least 70% by weight, particularly preferably in an amount of 80 to 100% by weight, based on the total weight of the crosslinking agent (F) set.
• polyepoxides (F2) are all known aliphatic and / or cycloaliphatic and / or aromatic polyepoxides, for example based on bisphenol-A or bisphenol-F.
• Suitable as component (F2) are, for example, those commercially available under the names Epikote®
• the polyepoxide component (F2) in the coating compositions according to the invention is advantageously present in an amount of 0 to 30% by weight, particularly preferably in an amount of 2 to 20% by weight, based on the
• suitable aminoplast resins (F3) are imino-functional melamine resins, such as the products commercially available under the name Cymel® 325 from Cyanamid and Luwipal® LR 8839 from BASF AG.
• the aminoplast resin (F3) is advantageously used in the coating compositions according to the invention in an amount of 0 to 30% by weight, particularly preferably in an amount of 2 to 20% by weight, based on the total weight of the crosslinking agent (F).
• the components (G) and (H) of the coating component (II) correspond to the components (C) and (E) of the coating component (I).
• (F) 50 to 100% by weight, preferably 60 to 90% by weight, at least one crosslinking agent (F),
• the components (J) and (K) of the coating component (III) correspond to the components (D) and (E) of the coating component (I).
• Components (IV) which consist of part or all of the auxiliaries and additives used in the coating composition are preferably used to produce the coating compositions according to the invention.
• Components (I) and (II) are preferably used for the production of the coating compositions in amounts such that the equivalent ratio of hydroxyl groups of the binder (A) to the crosslinking groups of the crosslinking agent (F) is between 1: 2 and 2: 1, preferably between 1: 1.2 and 1: 1.5.
• the coating compositions according to the invention also preferably have a total content of customary paint additives of 0 to 10% by weight, organic solvents of 5 to 25% by weight, preferably 10 to 20% by weight, of water of 25 to 70% % By weight, preferably from 30 to 60% by weight, of binder from 15 to 50% by weight, preferably from 20 to 40% by weight, of crosslinking agent from 5 to 30% by weight, preferably from 10 up to 20% by weight, and of pigments and / or fillers from 0 to 50% by weight, preferably from 0 to 30% by weight, in each case based on the total weight of the coating composition.
• Component (I) is prepared according to
• coloring pigments are usually incorporated by grinding (dispersing) the respective pigments in one or more binders.
• the pigments are rubbed in with the aid of conventional devices, such as, for example, pearl mills and sand mills.
• the effect pigments are usually incorporated by homogeneously mixing the effect pigments with one or more solvents. This mixture is then stirred into a mixture of one or more of the binders described above, if appropriate with the addition of further organic solvents, by means of a stirrer or dissolver.
• Components (II), (III) and optionally (IV) are likewise prepared by methods which are well known to the person skilled in the art by mixing or dispersing the individual constituents.
• the coating compositions according to the invention can be produced from components (I), (II), (III) and optionally (IV) by any conceivable mixing method. However, it is essential to the invention that components (I), (II), (III) and, if appropriate, (IV) are mixed and, if appropriate, dispersed only shortly before application of the coating compositions in the preparation of the coating compositions.
• components (I) and (II) in which case these components (I) and (II) preferably contain no neutralizing agent.
• component (IV) is optionally added to this mixture. Either the mixture thus obtained is then added to component (III) containing neutralizing agents and the coating agent obtained is dispersed. Or component (III) containing neutralizing agent is then added to the mixture thus obtained.
• coating composition according to the invention can be produced, for example, analogously to the process just described, although the neutralizing agent is not contained in component (III), but is added separately before component (III) is added.
• the coating composition according to the invention can also be prepared by component (I) the neutralizing agent is first added.
• component (I) which already contains the neutralizing agent.
• the component (I) thus obtained is then either
• Component (III) is added or component (III) is added, and the coating agent thus obtained is still homogenized by dispersing or
• Component (III) added and homogenized by dispersing and then the components (II) and optionally (IV) are added.
• the coating compositions of the invention are preferably prepared by mixing component (I) which has already been neutralized with component (II) and, if appropriate, component (IV) and then dispersing it into component (III).
• the coating compositions according to the invention can be applied by customary application methods, such as e.g. Spraying, knife coating, brushing, dipping, on any substrates, e.g. Metal, wood, plastic or paper can be applied.
• customary application methods such as e.g. Spraying, knife coating, brushing, dipping, on any substrates, e.g. Metal, wood, plastic or paper can be applied.
• the coating compositions according to the invention are usually cured at temperatures below 120 ° C., preferably at temperatures of at most 80 ° C.
• the coating compositions according to the invention are preferably used for the production of top coats.
• the coating compositions according to the invention can be used both in the series and also in the refinishing of automobile bodies. However, they are preferably used in the field of refinishing.
• aqueous coating compositions according to the invention can be used as fillers and for producing single-layer coatings
• Top coats and as pigmented basecoats or as clearcoats can be used in a process for producing a multi-layer paint system (base coat / clear coat process).
• the coating compositions according to the invention are preferably used as clear coats.
• the mixture (a1), (a2), (a3) and (a6) is added at such a rate that the addition is complete after 4 hours.
• the reaction mixture is kept at 120 ° C. for a further 2 h.
• the reaction mixture is adjusted to a solids content of 80% by distilling off the organic solvent.
• the acrylate resin thus obtained has an OH number of 140 mgKOH / g solid resin, an acid number of 40 mgKOH / g solid resin, a number average molecular weight of 2,800 and a weight average molecular weight of 8,700.
• the acrylic resin (VA1) is produced in the same way as the acrylic resin (AI). In contrast to the production of the acrylic resin (AI), however, after setting the solids content to 80% at 90 ° C., dimethylethanolamine (degree of neutralization: 85%) is first added and then adjusted to a solids content of 40% by adding water. The organic solvent is removed using Distillation removed in vacuo to 3% and a final solid of 40% is adjusted with water.
• the polyester resin is thinned with isopropoxypropanol to a solids content of 80%.
• the polyester thus obtained has an OH number of 130 mgKOH / g solid resin and a number average molecular weight of 1,500 and a weight average molecular weight of 3,800.
• the viscosity of a 50% solution of the polyester in ethoxyethyl propionate is 0.8 dPa-s (23 ° C). 4. Production of a Polyurethane Resin (A3) Used According to the Invention
• Pripol 1013 commercial dimer fatty acid with a monomer content of at most 0.1%, a trimers content of at most 2%, an acid number of 195 to 198 mg KOH / g and a saponification number of 198 - 202 mg KOH / g
• 107.7 g cyclohexanedimethanol 723.3 g hydroxipivalic acid neopentyl glycol ester, 17.2 g ethyl butyl propanediol, 392.6 g neopentyl glycol and 1018.7 g isophthalic acid with cyclohexane as entrainer and 0.25 g monobutyltin oxide hydrate implemented up to an acid number ⁇ 5.0.
• the cyclohexane was distilled off and the polyester was run up to an acid number of ⁇ 1.5.
• the mixture was cooled to about 100 ° C. and dissolved to 79.5% with ethoxyethyl propionate.
• the polyester diol B has an M n of 2352 (measured with GPC against the polystyrene standard) and a glass transition temperature (measured with DSC) of ⁇ 16 ° C.
• the viscosity of a 60% strength solution in ethoxyethyl propionent is 23 ° C. 3 , 5 dPa.s.
• the mixture was dissolved in 500 g of butoxypropanol and suddenly 23.9 g of dimethylethanolamine were added at a temperature of 100.degree. Finally, a solids content of 60% was set with butoxypropanol.
• the binder has an OH number of 60 mgKOH / g and an acid number of 20.6 mg KOH / g and a viscosity (10: 3 in N-methylpyrrolidone) of 13.5 dPa.s.
• the number average molecular weight is 4,500, the weight average molecular weight is 19,500.
• the viscosity of a 50% solution of the polyurethane in ethoxyethyl propionate is 4.1 dPa * s (23 ° C.).
• Component (I) is prepared from the constituents given in Table 1 by mixing using a stirrer (600 revolutions per minute).
• Component (II) is produced from the constituents given in Table 2 by mixing using a stirrer (600 revolutions per minute). 5.3. Preparation of component (III)
• Component (III) is prepared from the constituents given in Table 3 by mixing using a stirrer (600 revolutions per minute).
• the coating compositions of Examples 1 to 5 were produced by mixing the components given in Table 4 using a stirrer (600 revolutions per minute), by mixing components (I) and (II) to form component (III ) was added.
• Example 6 The coating compositions of Example 6 were prepared by mixing the components listed in Table 4 using a stirrer (600 revolutions per minute), by first premixing components (I) and (II) and then component (III) to this mixture was given.
• the coating compositions of Examples 7 to 9 were prepared analogously to the production of the coating compositions of Examples 2, 3 and 6, but with the difference that the components listed in Table 4 were processed manually, i.e. were mixed without using a stirrer.
• Example 10 The coating compositions of Example 10 were prepared by mixing the components given in Table 4 using a stirrer (600 revolutions per minute) by introducing component (III), then component (I) and then the component (II) was stirred.
• the coating compositions of Examples 11 to 14 were prepared by mixing the components listed in Table 5 using a stirrer (600 revolutions per minute), premixing components (I) and (II) and then adding them to component (III) ⁇ were stirred.
• the coating agent of Comparative Example 1 was produced analogously to the preparation of the coating agent of Example 1, with the difference that instead of the acrylate resin (AI) the acrylate resin (VA1) was used and that no component (III) was added.
• Component 1 was made from the following ingredients by mixing: 65 parts by weight of a commercially available polypropylene glycol with an average molecular weight of 400 and an OH number of 140 mg KOH / g (commercial product PPG-400 from Union Carbide)
• Component 1 was also prepared by the process described in the description of EP-A-368 499 in column 6, lines 45 to 50, by first processing the polypropylene glycol, the melamine-formaldehyde resin and the isopropanol into a mixture with stirring. The surface-active agent was then incorporated into this mixture with stirring.
• Component 2 was made from the following ingredients:
• Component 2 was produced analogously to the production of component 1 by the two processes described there.
• the applied base coating composition is dried for 10 minutes at room temperature and 10 minutes at 60 ° C.
• a top coating composition obtained in accordance with point 6 is applied to the base layer in 3 spray passes with an intermediate flash-off time of 15 minutes. splashes. Finally, it is dried for 60 minutes at room temperature and baked for 30 minutes at 60 ° C. in a forced air oven.
• the multilayer coatings thus obtained were subjected to several tests. The test results are shown in Tables 6 and 7.
• VA1 (FK: 39%) 1 ) - - - - - - - - - - - - 63.0
• non-ionic polyurethane thickener (10% in water) from Akzo
• test results (Examples 1-10) in Table 6 clearly show that the organically premixed components (I) and (II) produce better technological properties and wet climate pollution than mixing an aqueous component (I) with organic polyisocyanate (comparative example VI analogous to EP-B-0358 979).

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• 1994
  • 1994-06-22 DE DE4421823A patent/DE4421823A1/de not_active Withdrawn
• 1995
  • 1995-06-16 WO PCT/EP1995/002333 patent/WO1995035348A1/de not_active Application Discontinuation
  • 1995-06-16 ES ES95924253T patent/ES2132684T3/es not_active Expired - Lifetime
  • 1995-06-16 EP EP95924253A patent/EP0766717B1/de not_active Revoked
  • 1995-06-16 JP JP8501653A patent/JPH10501838A/ja not_active Ceased
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• 1996
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